Journal
CHEMISTRYSELECT
Volume 7, Issue 45, Pages -Publisher
WILEY-V C H VERLAG GMBH
DOI: 10.1002/slct.202203339
Keywords
hydrogen; nickel; Ni-0; Ni2+; steam methane reforming; water-gas shift reaction
Categories
Funding
- National Natural Science Foundation of China
- Haihe Laboratory of Sustainable Chemical Transformations
- [22178248]
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The Ni valence state on the surface of Ni/Al2O3 catalyst plays a crucial role in the catalytic performance of SMR. By tuning the Ni-0/Ni2+ ratio through reduction temperature control, the catalytic activity and selectivity of the catalyst can be greatly improved.
Steam methane reforming (SMR) is the most mature technology for hydrogen production in industry, and alumina supported nickel (Ni/Al2O3) is the most widely used catalyst. Herein, the key role of Ni valence state on the catalytic SMR performance of Ni/Al2O3 is reported. The ratio of Ni-0/Ni2+ on Ni/Al2O3 is individually and effectively tuned by changing the reduction temperature after wet impregnation. Catalytic performance of Ni/Al2O3 is greatly dependent on the surface concentration of Ni-0 and Ni2+. The catalyst reduced at 675 degrees C possesses balanced Ni-0 and Ni2+ sites and exhibits superior catalytic performance, on which 60 % of methane is stably converted at 600 degrees C. CH4-TPD and CO-TPD profiles demonstrate that appropriate Ni-0/Ni2+ ratio can promote the adsorption of CH4 and inhibit the moderate-strength adsorption of CO, which leads to increased SMR activity and selectivity.
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